U.S. patent application number 15/370372 was filed with the patent office on 2017-06-15 for system and method for fault diagnosis in emission control system.
The applicant listed for this patent is General Electric Company. Invention is credited to Sidharth ABROL, Sangeeta BALRAM, Prem Kumar PATCHAIKANI.
Application Number | 20170167349 15/370372 |
Document ID | / |
Family ID | 58773686 |
Filed Date | 2017-06-15 |
United States Patent
Application |
20170167349 |
Kind Code |
A1 |
BALRAM; Sangeeta ; et
al. |
June 15, 2017 |
SYSTEM AND METHOD FOR FAULT DIAGNOSIS IN EMISSION CONTROL
SYSTEM
Abstract
A fault detection method for a selective catalytic reduction
(SCR) system comprising an SCR reactor, includes receiving a
plurality of operating parameters (702) of the SCR reactor from a
plurality of sensors. The method also includes estimating a state
of an adaptive reactor model (704) representative of the SCR
reactor based on the plurality of operating parameters. The method
also includes generating a feature parameter (706) based on the
plurality of operating parameters and the estimated state of the
adaptive reactor model. The method includes determining a fault in
the SCR system (708) based on the feature parameter.
Inventors: |
BALRAM; Sangeeta;
(Bangalore, IN) ; ABROL; Sidharth; (Bangalore,
IN) ; PATCHAIKANI; Prem Kumar; (Bangalore,
IN) |
|
Applicant: |
Name |
City |
State |
Country |
Type |
General Electric Company |
Schenectady |
NY |
US |
|
|
Family ID: |
58773686 |
Appl. No.: |
15/370372 |
Filed: |
December 6, 2016 |
Current U.S.
Class: |
1/1 |
Current CPC
Class: |
F01N 2900/1616 20130101;
Y02T 10/12 20130101; B01D 53/9431 20130101; B01D 53/9495 20130101;
B01D 2257/404 20130101; F01N 2900/1812 20130101; F01N 2550/02
20130101; Y02T 10/24 20130101; Y02T 10/40 20130101; F01N 2900/08
20130101; F01N 2900/1411 20130101; F01N 2900/0404 20130101; Y02T
10/47 20130101; B01D 2251/2062 20130101; F01N 11/00 20130101; F01N
3/2066 20130101 |
International
Class: |
F01N 11/00 20060101
F01N011/00; B01D 53/94 20060101 B01D053/94; F01N 3/20 20060101
F01N003/20 |
Foreign Application Data
Date |
Code |
Application Number |
Dec 10, 2015 |
IN |
6607/CHE/2015 |
Claims
1. A fault detection method for a selective catalytic reduction
(SCR) system comprising an SCR reactor, the method comprising:
receiving a plurality of operating parameters of the SCR reactor
from a plurality of sensors; estimating a state of an adaptive
reactor model representative of the SCR reactor based on the
plurality of operating parameters; generating a feature parameter
based on the plurality of operating parameters and the estimated
state of the adaptive reactor model; and determining a fault in the
SCR system based on the feature parameter.
2. The method of claim 1, wherein the plurality of operating
parameters comprises one or more of a plurality of inlet
parameters, a plurality of outlet parameters, a reductant slip
value, an emission value, and a flow parameter.
3. The method of claim 1, wherein the adaptive reactor model
includes a time-varying mathematical model for the SCR reactor.
4. The method of claim 3, wherein the estimating comprises
determining estimates of states of the adaptive reactor model using
extended Kalman filtering.
5. The method of claim 1, wherein determining the fault comprises:
estimating a symptomatic parameter corresponding to a subsystem of
the SCR system using the adaptive reactor model using the plurality
of operating parameters; and determining the feature parameter
corresponding to the subsystem based on the symptomatic parameter
and the plurality of operating parameters.
6. The method of claim 5, wherein the symptomatic parameter
comprises at least one of an emission offset parameter and a
reductant slip offset parameter.
7. The method of claim 5, wherein the feature parameter comprises
at least one of an airflow offset, a reductant flow offset,
reductant valve offset, inlet emission offset, outlet emission
offset, and slip offset value.
8. The method of claim 5, wherein the subsystem comprises at least
one of an injection grid subsystem, a reactor inlet subsystem,
reactor subsystem and a reactor stack subsystem.
9. The method of claim 1, wherein the fault comprises at least one
of a blower fan fault, a flow sensor fault, a flow valve fault, an
inlet sensor fault, a stack sensor fault, a slip sensor fault, and
a catalyst fault.
10. A fault diagnosis system for a SCR system, comprising: a
selective catalytic reduction (SCR) reactor; a signal acquisition
unit; a plurality of sensors for providing a plurality of operating
parameters of the SCR reactor to the signal acquisition unit; an
emission control unit communicatively coupled to the signal
acquisition unit and configured to estimate states of an adaptive
reactor model representative of the SCR reactor based on the
plurality of operating parameters; a fault management unit coupled
to the SCR reactor and the emission control unit and configured to:
generate a plurality of feature parameters based on the plurality
of operating parameters and the adaptive reactor model; and
determine a fault in the SCR system based on the plurality of
feature parameters.
11. The system of claim 10, wherein the plurality of sensors are
configured to measure a plurality of inlet parameters, a plurality
of outlet parameters, a reductant slip value, an emission value and
a flow parameter.
12. The system of claim 10, wherein the adaptive reactor model
comprises a time-varying mathematical model for the SCR
reactor.
13. The system of claim 12, wherein the emission control unit is
configured to determine estimates of states of the adaptive reactor
model using extended Kalman filter (EKF).
14. The system of claim 10, wherein the fault management unit is
configured to: estimate a symptomatic parameter corresponding to a
subsystem of the SCR system using the adaptive reactor model using
the plurality of operating parameters; and determine a feature
parameter corresponding to the subsystem based on the symptomatic
parameter and the plurality of operating parameters.
15. The system of claim 14, wherein the fault management unit is
configured to determine at least one of an emission offset
parameter and a reductant slip offset parameter.
16. The system of claim 14, wherein the fault management unit is
configured to determine at least one of an airflow offset, a
reductant flow offset, reductant valve offset, inlet emission
offset, outlet emission offset, and slip offset value.
17. The system of claim 14, wherein the fault management unit is
configured to determine at least one of a fault in at least one of
an injection grid subsystem, a reactor inlet subsystem, reactor
subsystem and a reactor stack subsystem.
18. The system of claim 10, wherein the fault management unit is
configured to determine at least one of a plurality of faults
comprising a blower fan fault, a flow sensor fault, a flow valve
fault, an inlet sensor fault, a stack sensor fault, a slip sensor
fault, and a catalyst fault.
19. A non-transitory computer readable medium having instructions
to enable at least one processor unit to: receive a plurality of
operating parameters regarding a selective catalytic reduction
(SCR) reactor from a plurality of sensors; estimate states of an
adaptive reactor model representative of the SCR reactor based on
the plurality of operating parameters; generate a feature parameter
based on the plurality of operating parameters and the adaptive
reactor model; and determine a fault in a SCR system based on the
feature parameter.
Description
BACKGROUND
[0001] The invention relates generally to a technique for fault
diagnosis in emission control systems, and more particularly to a
technique for detecting faults in selective catalytic reduction
units.
[0002] Industrial emissions such as nitrogen oxides and sulphur
dioxide create environmental pollution. Environmental pollution is
regulated in most industries. Stringent regulation requirements are
being adopted by governments and standard bodies in order to
minimize the discharge of noxious gases into the atmosphere by
industrial facilities. Typically, an emission control system
includes a reduction reactor where the industrial emanations are
chemically treated with a reductant to reduce emissions.
Specifically, a reductant such as ammonia is injected into the
exhaust gas stream entering the reduction reactor to reduce
emissions such as NOx from the exhaust gas stream.
[0003] Analysis and control of exhaust emissions is performed to
comply with the regulation requirements. Emission analysis may be
performed continuously by using a gas composition analyzer
installed in the exhaust stack. Alternatively, the emission
analysis may be performed using the gas composition analyzer
connected to the exhaust stack through an extractive system.
However, continuous analysis is expensive due to installation cost,
maintenance and calibration requirements. A computer based model
may be used to predict emissions such as nitrogen oxide (NOx)
emission in order to reduce the cost of analysis of emissions. A
number of predictive parameters associated with the fuel conversion
process such as temperature and reductant coverage area are used by
the computer based model to determine an estimate of the amount of
the emissions.
[0004] Methodologies used in the past include nonlinear
statistical, neural network, eigenvalue, stochastic, and other
methods of processing the input parameters from available field
devices and to predict process emission rates and combustion or
process efficiency.
[0005] Emission control systems in power plants may experience
deterioration in performance and develop faults during operation.
Analysis based emission control techniques are not fully effective
in the presence of faults. Knowledge of faults may be used in
improvising the effectiveness of the emission control techniques.
Detection of faults also helps in foreseeing failure of components
and preparing for a planned maintenance schedule.
BRIEF DESCRIPTION
[0006] In accordance with one aspect of the present specification,
a fault detection method for a selective catalytic reduction (SCR)
system comprising an SCR reactor is disclosed. The method includes
receiving a plurality of operating parameters of the SCR reactor
from a plurality of sensors. The method further includes estimating
a state of an adaptive reactor model representative of the SCR
reactor based on the plurality of operating parameters. The method
also includes generating a feature parameter based on the plurality
of operating parameters and the estimated state of the adaptive
reactor model. The method includes determining a fault in the SCR
system based on the feature parameter.
[0007] In accordance with another aspect of the present
specification, a fault diagnosis system for a SCR system is
disclosed. The system includes a selective catalytic reduction
(SCR) reactor and a signal acquisition unit. The system further
includes a plurality of sensors for providing a plurality of
operating parameters of the SCR reactor to the signal acquisition
unit. The system also includes an emission control unit
communicatively coupled to the signal acquisition unit and
configured to estimate states of an adaptive reactor model
representative of the SCR reactor based on the plurality of
operating parameters. The system further includes a fault
management unit coupled to the SCR reactor and the emission control
unit and configured to generate a plurality of feature parameters
based on the plurality of operating parameters and the adaptive
reactor model. The fault management unit is also configured to
determine a fault in the SCR system based on the plurality of
feature parameters.
[0008] In accordance with another aspect of the present
specification, a non-transitory computer readable medium having
instructions is disclosed. The instructions enable at least one
processor unit to receive a plurality of operating parameters
regarding a selective catalytic reduction (SCR) reactor from a
plurality of sensors. The instructions further enable the at least
one processor to estimate states of an adaptive reactor model
representative of the SCR reactor based on the plurality of
operating parameters. The instructions also enable the at least one
processor to generate a feature parameter based on the plurality of
operating parameters and the adaptive reactor model. The
instructions further enable the at least one processor to determine
a fault in a SCR system based on the feature parameter.
DRAWINGS
[0009] These and other features and aspects of embodiments of the
present invention will become better understood when the following
detailed description is read with reference to the accompanying
drawings in which like characters represent like parts throughout
the drawings, wherein:
[0010] FIG. 1 is a diagrammatic illustration of a system for fault
diagnosis in emission control system, in accordance with aspects of
the present specification;
[0011] FIG. 2 is a signal flow diagram for the system of FIG. 1, in
accordance with aspects of the present specification;
[0012] FIG. 3 is a block diagram illustrating components of a
selective catalytic reduction (SCR) model, in accordance with
aspects of the present specification;
[0013] FIG. 4 is a graph illustrating performance of an embodiment
for estimating the SCR model, in accordance with aspects of the
present specification;
[0014] FIG. 5 illustrates an exemplary architecture for fault
diagnosis in an emission control system, in accordance with aspects
of the present specification;
[0015] FIG. 6 is a block diagram illustrating symptomatic
parameters, events and faults in a SCR system and their
interrelationships, in accordance with aspects of the present
specification; and
[0016] FIG. 7 is a flow chart of an exemplary method for fault
diagnosis in an emission control system, in accordance with aspects
of the present specification.
DETAILED DESCRIPTION
[0017] In certain embodiments, methods and systems for fault
diagnosis of an emission control system include receiving a
plurality of operating parameters from a selective catalytic
reduction (SCR) reactor and determining an SCR model based on the
plurality of operating parameters. A plurality of feature
parameters characterizing a plurality of operational events of the
SCR system is determined based on the plurality of operating
parameters and the SCR model. In instances where one or more faults
exist in the system, at least one of the one or more faults of the
SCR system is determined based on the plurality of feature
parameters.
[0018] The term "selective catalytic reduction (SCR) reactor" is
used to refer to a unit used to reduce emissions from an industrial
installation such as a power plant, an engine system, and a
production facility. The terms `SCR model` and the `reactor model`
are used equivalently and interchangeably to refer to a model
representative of the SCR reactor. The term "emissions" refers to
one or more or nitrogen oxide, nitrogen dioxide and used
equivalently and interchangeably with NOx. The term "reductant"
refers to a chemical such as ammonia used to reduce emissions from
the industrial installation through a chemical reduction process.
The term "emission control system" refers to a processor based
hardware element capable of determining an amount of the reductant
that is to be introduced into the SCR reactor for reducing the
emissions from a power plant to a desirable level. The term "fault"
refers to an operational defect in one or more subsystems or
components of the SCR system.
[0019] FIG. 1 illustrates a system 100 for fault diagnosis in a
power plant equipped with an emission control system 102. The
emission control system 102 includes a selective catalytic
reduction (SCR) reactor 108 coupled to an exhaust outlet 106, such
as a gas turbine exhaust configured to emanate an exhaust stream.
The SCR reactor 108 includes an inlet 114, an outlet 110 and a
catalyst 112 disposed inside the SCR reactor 108. The inlet 114 is
configured to receive the exhaust stream of the gas turbine exhaust
106 and the outlet 110 is configured to release treated emissions
to the atmosphere. The SCR reactor 108 also includes an injector
116 for introducing the reductant into the SCR reactor 108. The
reductant interacts with the emissions in the presence of catalyst
112 to generate treated emissions to be released to the
environment. The system 100 includes a signal acquisition unit 118,
an emission control unit 120, and a fault management unit 122. The
emission control unit 120 includes an adaptive reactor model 134.
The system 100 also includes a processor unit 124 and a memory unit
126.
[0020] The signal acquisition unit 118 is communicatively coupled
to the emission control system 102 and configured to obtain a
plurality of operating parameters 104 of the emission control
system 102. A plurality of sensors (not shown in FIG. 1) may be
employed by the emission control system 102 to measure the
plurality of operating parameters 104, for example. In one
embodiment, the plurality of sensors is disposed at the inlet 114
of the SCR reactor 108 and the outlet 110 of the SCR reactor 108
for providing a plurality of operating parameters to the signal
acquisition unit 118. In one embodiment, the plurality of
parameters includes a plurality of inlet parameters of the SCR
reactor 108, a plurality of outlet parameters of the SCR reactor
108, a reductant slip value acquired from the outlet 110, an
emission value from the SCR reactor 108, and a flow parameter
representative of a reductant inflow into the SCR reactor 108. The
plurality of inlet parameters may include, but is not limited to,
ammonia (NH.sub.3), Oxygen (O.sub.2), nitrogen monoxide (NO),
nitrogen dioxide (NO.sub.2). The plurality of outlet parameters may
include, but is not limited to, a slip value and an emission value
measured at the outlet 110 of the SCR reactor 108. The signal
acquisition unit 118 may also be configured to retrieve a slip
set-point from a pre-determined memory location in the system 100.
In one embodiment, the slip set-point is determined by offline
experiments and is stored in the memory unit 126 that may be
accessible by the signal acquisition unit 118. In one embodiment,
the plurality of inlet parameters and the plurality of outlet
parameters are obtained from Continuous Emission Monitoring System
CEMS).
[0021] The emission control unit 120 is communicatively coupled to
the signal acquisition unit 118 and configured to receive the
plurality of operating parameters 104 from the signal acquisition
unit 118. The emission control unit 120 is configured to estimate
an adaptive reactor model 134 representative of the SCR reactor 108
based on the plurality of operating parameters. The adaptive
reactor model 134 is configured to simulate chemical reactions of
the SCR reactor and generate estimates of a plurality of operating
parameters. In one embodiment, the adaptive reactor model 134 is a
time-varying non-linear model operating in a plurality of states. A
state of the adaptive reactor model refers to a combination of
operating parameters of the adaptive reactor model at a specific
time instant. The estimation of the adaptive reactor model 134 by
the emission control unit 120 includes determining one or more
parameters of the adaptive reactor model 134 in real time. In one
embodiment, estimating the adaptive reactor model 134 includes
estimating states based on the plurality of operating parameters.
In some embodiments, the emission control unit 120 is further
configured to estimate a reductant flow set-point based on the
adaptive reactor model 134 and the plurality of operating
parameters. The reductant flow set point is provided to the
injector 116 for controlling the flow of the reductant into the SCR
reactor 108. By way of example, the reductant flow set point may be
provided to the injector 116 using automatic control by the
emission control unit 120 or manual control to facilitate reduction
of emanations from the outlet 110 of the SCR reactor 108. In case
of the manual control, an operator may manually set a reductant
valve to facilitate reduction of emanations from the outlet 110 of
the SCR reactor 108. The emission control unit 120 may be used by
the operator in estimating the reductant flow set-point retrieved
by a memory location.
[0022] In one embodiment, the adaptive reactor model 134 includes a
time-varying mathematical model for the SCR reactor. In another
embodiment, the adaptive reactor model 134 is based on a dynamic
response of at least one of the plurality of sensors. As an
example, the time-varying mathematical model includes an extended
Kalman filter (EKF). In another example, the time-varying
mathematical model may include other filtering techniques based on
filters such as such as Kalman filter and its variants such as
unscented Kalman filter (UKF). The time-varying mathematical model
is configured to adaptively estimate states of the adaptive reactor
model in real time.
[0023] The adaptive reactor model 134 may include electronics
(hardware and/or software) capable of performing operations
including but not limited to signal decoding and/or delay
insertion. In a non-limiting example, to aid in the above mentioned
operations, the adaptive reactor model 134 may include a
microprocessor, memory, or combinations thereof. The microprocessor
may include a reduced instruction set computing (RISC) architecture
type microprocessor or a complex instruction set computing (CISC)
architecture type microprocessor. Further, the microprocessor may
be of a single-core type or multi-core type.
[0024] The fault management unit 122 is coupled to the emission
control unit 120 and configured to detect a fault of the SCR
reactor 108. In embodiments where one or more faults are detected,
the fault management unit 122 may provide suggestions to an
operator for managing and correcting the faults. Further, the fault
management unit 122 is configured to estimate a symptomatic
parameter corresponding to a subsystem of the emission control
system 102 based on the reactor model 134 and a plurality of
operating parameters. In one embodiment, the symptomatic parameter
includes at least one of the emission offset and a reductant slip
offset parameter. The term "emission offset" refers to a difference
between the emission values from the outlet 110 and an estimate of
the emission value from the SCR model. Similarly, the term
"reductant slip offset" refers to a difference between the
reductant flow set point value and the actual reductant flow
measured by a sensor. It should be noted herein that the
symptomatic parameter may also include one of the plurality of
operating parameters. The fault management unit 122 is also
configured to determine a plurality of feature parameters
corresponding to at least one subsystem of the emission control
system 102 based on the symptomatic parameter and the plurality of
operating parameters. The at least one subsystem of the emission
control system 102 may include at least one of an injection grid
subsystem, a reactor inlet subsystem, a reactor catalyst subsystem,
a reactor subsystem, a reactor stack subsystem, and a Heat Recovery
Steam Generator (HRSG) stack subsystem. The plurality of feature
parameters may be used to identify operational events of the SCR
reactor 108. The plurality of feature parameters comprises
characteristic parameters capable of determining a plurality of
events during the operation of the emission system and may include,
for example at least one of an airflow offset, a reductant flow
offset, a reductant valve offset, an inlet emission offset, an
outlet emission offset, and a slip offset value.
[0025] The plurality of feature parameters is related to at least
one of the subsystems. The operational events determined based on
the plurality of feature parameters are indicative of an
operational state of an associated subsystem. Further, the
operational events may be used by the fault measurement unit 122 to
generate a fault indicator 128. As an example, a flow sensor fault
is determined by detecting an operational event, such as a
reductant flow event. Further, the reductant flow event in turn is
determined based on the feature parameter, such as the reductant
flow offset. The plurality of faults detected by the exemplary
techniques disclosed herein includes, but is not limited to, a
blower fan fault, a flow sensor fault, a flow valve fault, an inlet
sensor fault, a stack sensor fault, a slip sensor fault, and a
catalyst fault.
[0026] In the system 100, the processor unit 124 is communicatively
coupled to the communication bus 130 and may include at least one
arithmetic logic unit, a microprocessor, a general purpose
controller, or a processor array to perform the desired
computations or run the computer program. In one embodiment, the
functionality of the processor unit 124 may be limited to tasks
performed by the signal acquisition unit 118. In another
embodiment, the functionality of the processor unit 124 may be
based on the functions performed by the emission control unit 120.
In yet another embodiment, the functionality of the processor unit
124 may be based on the functions performed by the fault management
unit 122. The processor unit 124 may be configured to provide the
functionality of one or more of the signal acquisition unit 118,
the emission control unit 120, and the fault management unit 122.
While the processor unit 124 is shown as a single unit, it may be
noted that the processor unit 124 may be present in the system 100
as two or more units, where each unit of the two or more units may
include one or more processors that are configured to provide the
functionality of one or more of the signal acquisition unit 118,
the emission control unit 120, and the fault management unit
122.
[0027] Further, the memory unit 126 of the system 100 is
communicatively coupled to the processor unit 124 and is configured
to be accessed by at least one processor residing in at least one
of the units 118, 120 and 122. In an exemplary embodiment, the
memory unit 126 may refer to one or more memory modules. The memory
unit 126 may be a non-transitory storage medium. For example, the
memory unit 126 may be a dynamic random access memory (DRAM)
device, a static random access memory (SRAM) device, flash memory
or other memory devices. In one embodiment, the memory may include
a non-volatile memory or similar permanent storage device, media
such as a hard disk drive, a floppy disk drive, a compact disc read
only memory (CD-ROM) device, a digital versatile disc read only
memory (DVD-ROM) device, a digital versatile disc random access
memory (DVD-RAM) device, a digital versatile disc rewritable
(DVD-RW) device, a flash memory device, or other non-volatile
storage devices. In one specific embodiment, a non-transitory
computer readable medium may be encoded with a program having
instructions to instruct at least one processor to perform
functions of one or more of the signal acquisition unit 118, the
emission control unit 120, and the fault management unit 122.
[0028] FIG. 2 illustrates a signal flow diagram 200 for the fault
diagnosis system 100 of FIG. 1. The signal flow diagram 200
includes an SCR system 226 having a gas turbine inlet, an exhaust
outlet, and a SCR reactor in between the inlet and the outlet.
Emissions from the SCR system are monitored and controlled by an
emission control unit 202 having an adaptive reactor model 214
representative of the SCR reactor. A fault management unit 212 is
communicatively coupled to the emission control unit and the SCR
system 226 and configured to determine a plurality of faults
220.
[0029] A plurality of sensors are disposed in the SCR system 26 and
configured to measure a plurality of operating parameters 206. The
plurality of operating parameters 206 typically includes a
plurality of inlet parameters measured at the inlet of the SCR
system 226 and also a plurality of outlet parameters measured at
the exhaust of the SCR system 226. The plurality of operating
parameters 206 may be used by the emission control unit 202, the
adaptive reactor model 214, and/or the fault management unit 212.
The emission control unit 202 is also configured to receive a
feedforward signal 204 representative of an estimate of residual
reductant in the SCR reactor and a feedback signal 210
representative of the reductant slip value from the exhaust of the
SCR system 226. The emission control unit 202 is also configured to
receive estimates of the plurality of operating parameters from the
adaptive reactor model 214. The emission control unit 202 is
configured to estimate states 208 of the SCR reactor. Further, the
emission control unit 202 is also configured to estimate a
reductant flow set-point 224 to be provided to an injection
subsystem of the SCR system 226. In one embodiment, the reductant
set point 224 is determined based on the feedforward signal 204 and
the feedback signal 210. In one embodiment, an extended Kalman
filter is used to determine the states 208 of the SCR reactor
model. In one embodiment, estimates of plurality of operating
parameters of the SCR system 226 is obtained from the adaptive
reactor model 214.
[0030] The fault management unit 212 is configured to receive the
plurality of operating parameters 206 and the states 208 of the
adaptive reactor model. The fault management unit 212 is also
configured to exchange fault related information 222 with the SCR
reactor 226. The fault management unit 212 is configured to
generate a plurality of symptomatic parameters 216 based on the
plurality of parameters 206. The fault management unit 212 is
further configured to generate a plurality of feature parameters
218 based on the plurality of symptomatic parameters 216. The fault
management unit 212 is further configured to determine a plurality
of events representative of a plurality of faults 220 based on the
plurality of symptomatic parameters 216 and the plurality of
feature parameters 218.
[0031] FIG. 3 is a block diagram illustrating components of a
mathematical model 300 for a SCR model located in the emission
control unit 120 of FIG. 1. The mathematical model 300 is a kinetic
model representative of chemical reactions that take place in the
SCR unit. In the SCR unit, ammonia is injected from the injector
into the exhaust gas stream and may react, in the presence of the
catalyst, with NOx to produce nitrogen (N.sub.2) and water
(H.sub.2O). The chemical reactions include, but are not limited to,
ammonia adsorption and desorption reaction with the catalyst,
ammonia oxidation reaction, standard SCR reaction, fast SCR
reaction, NO.sub.2 SCR reaction, and NO oxidation reaction. The
mathematical model 300 includes a set of algebraic equations 304,
306, 308 and a set of ordinary differential equations 310
characterizing reactions within the SCR reactor. The set of
algebraic equations includes a plurality of rate equations 304
describing characteristics of the individual reactions such as
concentration change of each chemical reactant or product. The set
of algebraic equations also include equations for catalyst
temperature 306, mass balance equation on ammonia, nitrogen oxide,
and nitrogen dioxide 308. The set of ordinary differential
equations 310 include equations for mass balance on ammonia surface
coverage. The SCR model includes a plurality of parameters such as
chemical composition and concentration of each chemical reactant or
product and the coverage ratio of ammonia on the catalyst. The
coverage ratio of ammonia on the catalyst may further depend at
least on the characteristics of the catalyst, such as chemical
composition, catalyst substrate, physical geometry, and the time of
usage.
[0032] FIG. 4 is a graph 400 illustrating the performance of a
technique for estimating the SCR model. The graph 400 includes an
x-axis 402 representative of time in minutes and a y-axis 404
representative of emissions at SCR outlet in parts per million.
Curves 406, 408, 410 are representative of emission values obtained
from the SCR unit, and corresponding estimates obtained from two
different models respectively. The curve 406 represents
measurements of emissions at outlet of the SCR unit. The curve 408
is representative of estimates of the emissions obtained from a SCR
model without any state estimation technique. The curve 410 is
representative of estimates of the emissions obtained from the SCR
model using an extended Kalman filter. It may be observed that the
curves 408 and 410 match closely compared to the curve 406.
[0033] FIG. 5 illustrates architecture 500 for fault diagnosis in
an emission control system, such as the emission control unit 120
of FIG. 1. The architecture 500 includes two categories of control
units, namely a SCR control unit 502 and a gas turbine control unit
504, corresponding to the SCR unit and an exhaust generator (such
as a gas turbine), respectively. The SCR control unit 502 includes
ammonia control valve 506, an atomized air control valve 508, and
dilution fans 510 controlling the operation of a vaporizer that
feeds the reductant flow to the injection grid 514. The gas turbine
control unit 504 includes mechanisms for fuel split, a fuel stroke
reference (FSR) position, and an inlet bleed heating system (IBH)
controlling the operation of the gas turbine (GT) system 512. The
plurality of sensors includes, but is not limited to, a reductant
flow sensor measuring reductant flow into the SCR reactor, SCR
inlet sensor for measuring inlet emissions, emission sensor for
measuring emission from the outlet, and a slip sensor measuring the
residual reductant from the outlet of the SCR system.
[0034] A plurality of operating parameters 522 include, but is not
limited to, FCV (Flow Control Valve--Position), F.sub.E (Flow
Element--Flow through Control Valve), P (Pressure), T
(Temperature). F.sub.exh (Flow from gas turbine exhaust), O.sub.2
(Oxygen Percentage), CO (Carbon Monoxide--ppm), measurements of NO,
NO.sub.2 and NH3 obtained from the CEMS (Continuous Emission
Monitoring System). The plurality of operating parameters 522 may
be used to detect one or more symptomatic parameters that are
indicative of a fault in the emission control system. The emission
control system includes a plurality of subsystems such as the
injection grid 514, a SCR inlet 516, a SCR catalyst 518, and a HRSG
520. The fault diagnosis architecture 500 includes a plurality of
techniques 524 for determining at least one event associated with
one or more of the subsystems 514, 516, 518, and 520. The at least
one event is determined based on one or more symptomatic
parameters. A fault condition of the emission control system,
associated with a particular subsystem may be determined based on
the one or more symptomatic parameters and at least one of the
detected events.
[0035] FIG. 6 is a block diagram 600 illustrating a relationship
between a plurality of symptomatic parameters 602 indicative of
symptoms of one or more faults in the emission control system, a
plurality of events 604 associated with faults, and a plurality of
faults 606 associated with specific subsystem in a SCR emission
control system. In an exemplary embodiment, the plurality of
symptomatic parameters include, but are not limited to, a decreased
stack emission reduction 608, and an increased stack ammonia slip
value 610. A plurality of offset values is determined based on the
plurality of operating parameters in each of the subsystems. For
example, corresponding to the injection grid subsystem, an air
atomization offset, a blower speed offset, a reductant flow offset,
and a reductant valve offset may be determined based on the
operating parameters. In another example, an inlet emission offset
may be determined corresponding to the SCR inlet subsystem. In
another example, an outlet emission offset, and a slip offset may
be determined based on the plurality of operating parameters
corresponding to the SCR catalyst subsystem and SCR stack
subsystem.
[0036] The air atomization offset refers to an offset between
actual and desired positions of an air atomization actuator. The
blower speed offset refers to a difference between an actual blower
speed and a desirable blower speed. The term "reductant flow
offset" refers to a difference between an actual reductant flow
measured from a reductant sensor and an estimate of the required
reductant flow as estimated by the emission control unit 120 of
FIG. 1. The term "reductant valve offset" refers to a difference
between a reductant demand estimated by the SCR model and the
actual reductant flow determined based on a flow valve position.
The term "inlet emission offset" refers to a difference between an
emission estimate corresponding to a gas turbine and a HRSG based
on a gas turbine model and actual measurements of emissions
provided to the SCR inlet by the exhaust outlet 106. The term
"outlet emission offset" refers to a difference between emissions
estimated by the SCR model and emissions measured at the outlet of
the SCR unit. The terms "outlet emission offset" and "emission
offset" are used interchangeably and equivalently in this
specification. The term "slip offset value" refers to a difference
between a slip value estimated by the SCR model and the measured
slip value.
[0037] A plurality of events indicative of a plurality of faults
associated with the emission control system may be determined based
on the plurality of offset values. A plurality of threshold values
are used with the plurality of offset values to determine the
plurality of faults. In a first step, when an offset value exceeds
a corresponding predetermined threshold value, a corresponding
event is detected. Further, when the corresponding event is
detected, a fault associated with the detected event is identified
as being present in the emission control system. The plurality of
events associated with the plurality of subsystems include, but are
not limited to, air atomization event and a blower speed event 612,
a reductant flow event 614, a reductant demand event 616, an inlet
emission event 618, an outlet emission event 620, and a slip offset
event 622. The plurality of faults determined by an exemplary
technique includes, but are not limited to, air atomization control
valve fault (and a blower fan fault) 624, a flow sensor fault 626,
a flow valve fault 628, an inlet sensor fault 630, a stack sensor
fault 632, a slip sensor fault 634, and a catalyst fault 636.
[0038] In one example, one or more faults associated with the
injection grid subsystem are determined. By way of example, when
the air atomization offset value exceeds an atomization threshold
value, an air atomization event is detected and a fault in control
valve used for air atomization is detected. In another example,
when the blower speed offset exceeds a blower offset threshold
value, a blower speed event is detected and a blower fan fault is
detected. When the reductant flow offset value exceeds a reductant
flow threshold value, the reductant flow event is detected and a
flow sensor fault is detected. When the reductant valve offset
exceeds a reductant valve threshold value, the reductant demand
event is detected and a flow control valve fault is detected
[0039] In another example, faults associated with the SCR inlet
subsystem are determined. Specifically, when an inlet emission
offset exceeds an inlet emission threshold value, the inlet
emission event is detected and an SCR inlet sensor fault is
detected. Further, in one example, one or more of faults associated
with the SCR catalyst subsystem are determined. Specifically, when
the slip offset exceeds a slip threshold value, a slip event is
detected and a slip sensor fault is detected. When the outlet
emission offset exceeds an outlet emission threshold value, an
outlet emission event is detected and an emission sensor fault is
detected. If the slip event and the outlet emission events are
simultaneously detected, catalyst fault is detected.
[0040] In one embodiment, the plurality of threshold values such as
the atomization threshold value, the blower offset threshold value,
the reductant flow threshold value, the reductant valve threshold
value, the inlet emission threshold value, the slip threshold
value, and the outlet emission threshold value are determined
apriori and stored in memory locations. In another embodiment, the
plurality of threshold values may be provided by an operator of the
system. In one embodiment, rate of change of offset values are also
used in determining the plurality of faults. In another embodiment,
a time duration for which one of a plurality of thresholds exceed a
corresponding offset value is used for determining a fault
condition. In one embodiment, the catalyst fault is detected using
additional values of slip threshold value and outlet emission
threshold values.
[0041] FIG. 7 is a flow chart 700 illustrating steps of a method
for fault diagnosis in emission control system. The method includes
receiving a plurality of operating parameters from a plurality of
sensors disposed in inlet of a SCR unit in step 702. The sensors in
the plurality of sensors include, but are not limited to, a
reductant flow sensor, a SCR inlet sensor, an emission sensor, a
slip sensor, or combinations thereof. The plurality of operating
parameters include a plurality of inlet parameters such as
reductant flow rate, a plurality of outlet parameters such as
emission from the exhaust, and other parameters such as pressure,
temperature, oxygen, flow reading from flow control value, FCV, FE,
P, T. Fexh, O.sub.2, CO, measurements of NO, NO.sub.2 and NH.sub.3
obtained from the CEMS. At step 704, the method further includes
estimating an adaptive reactor model representative of the SCR
reactor based on the plurality of operating parameters. The
adaptive reactor model is based on a set of mathematical equations
representative of chemical reactions within the SCR unit. A state
estimation technique such as extended Kalman filter (EKF) is used
to update the adaptive reactor model in real time. At step 706, a
plurality of estimated operating parameters is determined based on
the adaptive reactor model. Further, a plurality of offset values
are determined based on the plurality of estimated operating
parameters. At step 708, a fault of the emission control system is
determined based on the offset value and the adaptive reactor
model.
[0042] As an example, a reductant slip offset parameter is compared
with a reductant slip threshold value to detect a symptom of a
fault. When the symptom of a fault is detected, a plurality of
offset values related to the plurality of subsystems of the SCR
reactor are determined and compared with respective offset
threshold values. If air atomization offset value exceeds an
atomization threshold value, an air atomization event is detected
and a fault in control valve used for air atomization is
detected.
[0043] It is to be understood that not necessarily all such objects
or advantages described above may be achieved in accordance with
any particular embodiment. Thus, for example, those skilled in the
art will recognize that the systems and techniques described herein
may be embodied or carried out in a manner that achieves or
improves one advantage or group of advantages as taught herein
without necessarily achieving other objects or advantages as may be
taught or suggested herein.
[0044] While the technology has been described in detail in
connection with only a limited number of embodiments, it should be
readily understood that the specification is not limited to such
disclosed embodiments. Rather, the technology can be modified to
incorporate any number of variations, alterations, substitutions or
equivalent arrangements not heretofore described, but which are
commensurate with the spirit and scope of the claims. Additionally,
while various embodiments of the technology have been described, it
is to be understood that aspects of the specification may include
only some of the described embodiments. Accordingly, the
specification is not to be seen as limited by the foregoing
description, but is only limited by the scope of the appended
claims.
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